A kind of preparation method of peony seed oil
(1) technical field
The invention belongs to edible oil processing technique field, particularly a kind of preparation method of peony seed oil.
(2) background technology
Tree peony is wide in China's cultivated area, and especially Shandong, Henan, Anhui, wherein based on Luoyang, Heze, Tongling.Peony seed oil contains various active composition, wherein unsaturated fatty acid content is up to more than 80%, linoleic acid content is more than 42%, it is " edible oil star---sweet oil " at present more than 40 times, there is the title of skin " caregiver " and " blood vessel bodyguard ", based on these high nutritive values, and there is the regional color of raw material, within 2011, be approved as national new resource food by health ministry.
Chinese invention patent CN103416490A discloses the technology that a kind of milling process extracts peony seed oil, adopt aquation combined acid to come unstuck to carry out peony seed oil to come unstuck, but the method oil yield is low, and what take when refining is conventional process flow: come unstuck, depickling, decolouring, deodorization.Present inventor, through great many of experiments, finally invents a kind of preparation method of efficient, high-quality, the simple peony seed oil of technique.
(3) summary of the invention
The present invention, in order to make up the deficiencies in the prior art, provides a kind of preparation method shortening extraction time, improve product quality, be applicable to the peony seed oil of suitability for industrialized production.
The present invention is achieved through the following technical solutions:
A preparation method for peony seed oil, take peony seeds as raw material, comprises the steps:
(1) peony seeds removed the peel, pulverize as peony seeds powder, in drying process, make its biodiversity content be reduced to 10-15%;
(2) peony seeds powder is put into ultrahigh pressure vessel, carry out ultra-high voltage and assist normal hexane to carry extraction using alcohol secretly, obtain peony seed oil extracting solution, peony seed oil extracting solution is carried out suction filtration and obtains coarse wool oil, vacuum tightness is 0.08-0.1MPa;
(3) coarse wool oil is transferred in round-bottomed flask, in Rotary Evaporators, carries out concentrating under reduced pressure, successively reclaim normal hexane and ethanol;
(4) the coarse wool oil after concentrated is transferred in centrifuge tube, centrifugally comes unstuck, obtain crude oil clearly;
(5) heat clear crude oil to 60-70 DEG C, add sodium hydroxide solution, centrifugally remove soap stock;
(6) the clear crude oil after centrifugal is imported bleacher, add the activated decoloration accounting for crude oil weight 3-4% clearly, bleacher is vacuumized simultaneously, bleaching temperature is controlled at 90-110 DEG C, stir decolouring;
(7) by the clear crude oil vacuum pump suction filtration of decolouring, vacuum tightness is 0.085-0.09MPa;
(8) the clear crude oil after suction filtration is proceeded to Rotary Evaporators, be warming up to 120-170 DEG C, distillation 3-6 hour, then vacuumizes, cools, and obtains refining peony seed oil product.
Peony seeds benevolence is pulverized by the present invention, and then carry out vacuum-drying to peony seeds powder, drying efficiency is high, effective, ensures the quality of peony seed oil from raw material; Ultra-high voltage is assisted normal hexane to carry Ethanol Method solvent extraction secretly and is only needed 20 minutes, extraction time is short, the crude oil obtained is after centrifugal, can complete and come unstuck, and ethanol both can dephosphorization fat, again can deproteinated, can realize " coming unstuck in Ti You limit, limit ", and more thorough than " traditional hydration degum " method, better effects if.
In step (1), peony seeds peeler is removed the peel, through screening, obtain peony seeds benevolence, peony seeds benevolence is pulverized, with 40 eye mesh screen screenings, the peony seeds powder sieved is sent into vacuum drying oven inner drying, every 2min stirs peony seeds powder, and time of drying is 15-20 minute, and the biodiversity content processed to peony seeds powder is 10-15%; Can drying efficiency be improved like this, energy-and time-economizing, the cause thermal damage that peony seeds powder is caused because local superheating causes can also be avoided, ensure the quality of peony seed oil from raw material.
In step (2), the solid-liquid ratio of peony seeds powder, normal hexane and ethanol is 1g:13-15mL:4-6mL, normal hexane and ethanol are placed in vacuum packaging bag, again peony seeds powder is imported in vacuum packaging bag and mix, vacuum-sealing, extraction pressure is 500-550MPa, and the dwell time is 15-20min, temperature is 50 DEG C, obtains peony seeds extracting solution; Solid-liquid ratio is according to calculation formula
v=
m×
w×
a, draw in conjunction with great many of experiments, wherein simultaneously
vfor the addition (mL) of water,
mfor the quality (g) of peony seeds powder,
wfor oil length,
afor experience factor 4-6%.
In step (3), first 40 DEG C, vacuum tightness reclaims normal hexane under being 0.08MPa condition, drip to prolong place absence of liquid, after be warming up to 45 DEG C, keeps vacuum tightness 1-2 hour constant, continue concentrated, recovery ethanol.
In step (4), the rotating speed of centrifuge tube is 5000-5500r/min, centrifugal 20min.
In step (6), stirring bleaching time is 30min.
In step (8), the pumpdown time is 3-4 hour, and vacuum tightness is 0.06-0.09MPa, vacuumizes rear valve-off, opens coolant valve, is cooled to 40-60 DEG C, obtains product.
The ultra-high voltage that the present invention adopts has the advantages that to destroy plant tissue, the solubility rate of the natural antioxidants vitamins C in peony seeds and tocopherol can be made higher, make extracted peony seed oil possess better antioxidative stabilizer, namely possess better storage stability.
Present invention process flow process is simple, and extraction time is short, and the peony seed oil extraction yield of extraction is up to 30-31.5%, and in peony seed oil after refining, linolenic acid content accounts for the ratio of lipid acid up to 60%() left and right, superior product quality, is suitable for wide popularization and application.
(4) embodiment
Below in conjunction with embodiment, the present invention is described in further detail, but does not therefore limit the present invention among described scope of embodiments.
Embodiment 1:
The preparation method of peony seed oil, to the steps include: featured peony seeds through crushing and screening, dry, extract, filter, concentrated, depickling, decolouring, deodorization thus obtain refining peony seed oil.Processing parameter important in its step is: existing peony seeds powder was pulverized 40 mesh sieves, after dry in vacuum drying oven, dry 15-20 minute, the biodiversity content processed to peony seeds benevolence is 10%-15%.Adopt ultra-high voltage secondary solvent to carry Ethanol Method secretly to extract, organic solvent used is normal hexane and ethanol, solid-liquid ratio is 1:15:6 (peony seeds powder quality: normal hexane volume: ethanol contend, g:mL:mL), and normal hexane and ethanol are placed in vacuum packaging bag, after peony seeds powder poured in evacuated panel pack, mixing, vacuum-sealing, extraction pressure setting is 500MPa, dwell time is 20 minutes, and temperature is 50 DEG C; After extracting solution is proceeded in suction filtration machine, vacuum tightness is 0.1-0.08 MPa, gained crude oil is transferred in cleaning, dry round-bottomed flask, in Rotary Evaporators, carry out underpressure distillation concentrate, first 40 DEG C, vacuum tightness reclaims normal hexane under being 0.08MPa condition, drip to prolong place absence of liquid; After be warming up to 55 DEG C, keep vacuum tightness 1-2 hour constant, continue concentrated, reclaim ethanol.To proceed in whizzer through concentrated peony seeds crude oil, rotating speed is 5500r/min, and centrifugal 20 minutes, supernatant liquor was the crude oil that comes unstuck; Use alkali-refining deacidification, caustic dosage is alkali number and excess alkali quantity sum, and concentration of lye is 10%, alkali refining initial temperature is 40 DEG C, stirring velocity 50r/min when adding alkali, when oily soap is separated, reduce stirring velocity, under 5500r/min, carry out centrifugal 15 minutes, remove soap stock, obtain depickling oil; By above-mentioned through coming unstuck, depickling crude oil import bleacher, add and account for the activated decoloration that crude oil weighs 3%, bleacher is vacuumized simultaneously, bleaching temperature is controlled at 90 ~ 110 DEG C, stir decolouring about 30 minutes; During vacuum deodorization, the decolouring crude oil after filtering is proceeded to Rotary Evaporators, is warming up to 120-170 DEG C, distillation 2-5 hour, vacuumize 4 hours, vacuum tightness is 0.06-0.09MPa, vacuumizes rear valve-off, open coolant valve, be cooled to about 40 DEG C, obtain refining peony seed oil.
Embodiment 2:
The preparation method of peony seed oil, to the steps include: featured peony seeds through crushing and screening, dry, extract, filter, concentrated, depickling, decolouring, deodorization thus obtain refining peony seed oil.Processing parameter important in its step is: existing peony seeds powder was pulverized 40 mesh sieves, after dry in vacuum drying oven, dry 15 minutes, the biodiversity content processed to peony seeds benevolence was 10%.Adopt ultra-high voltage secondary solvent to carry Ethanol Method secretly to extract, organic solvent used is normal hexane and ethanol, solid-liquid ratio is 1:13:4 (peony seeds powder quality: normal hexane volume: ethanol contend, g:mL:mL), and normal hexane and ethanol are placed in vacuum packaging bag, after peony seeds powder poured in evacuated panel pack, mixing, vacuum-sealing, extraction pressure setting is 550MPa, dwell time is 15 minutes, and temperature is 50 DEG C; After extracting solution is proceeded in suction filtration machine, vacuum tightness is 0.1-0.08MPa, removes peony seeds residue; Gained crude oil is transferred in cleaning, dry round-bottomed flask, in Rotary Evaporators, carries out underpressure distillation concentrate, first 40 DEG C, vacuum tightness reclaims normal hexane under being 0.08MPa condition, drip to prolong place absence of liquid; After be warming up to 45 DEG C, keep the vacuum constant 1-2 hour, continues concentrated, reclaims ethanol.To proceed in whizzer through concentrated peony seeds crude oil, rotating speed is 5000r/min, and centrifugal 20 minutes, supernatant liquor was the crude oil that comes unstuck; Use alkali-refining deacidification, caustic dosage is alkali number and excess alkali quantity sum, and concentration of lye is 10%, alkali refining initial temperature is 40 DEG C, stirring velocity 60r/min when adding alkali, when oily soap is separated, reduce stirring velocity, under 5500r/min, carry out centrifugal 15 minutes, remove soap stock, obtain depickling oil; By above-mentioned through coming unstuck, depickling crude oil import bleacher, add and account for the activated decoloration that crude oil weighs 4%, bleacher is vacuumized simultaneously, bleaching temperature is controlled at 90-110 DEG C, stir decolouring about 30 minutes; During vacuum deodorization, the decolouring crude oil after filtering is proceeded to Rotary Evaporators, is warming up to 120-170 DEG C, distillation 2-5 hour, vacuumize 4 hours, vacuum tightness is 0.06-0.09MPa, vacuumizes rear valve-off, open coolant valve, be cooled to about 60 DEG C, obtain refining peony seed oil.